NO149957B - PROCEDURE FOR PREPARING 4- (6`-METOXY-2`-NAPHYL) BUTAN-2-ON - Google Patents

PROCEDURE FOR PREPARING 4- (6`-METOXY-2`-NAPHYL) BUTAN-2-ON Download PDF

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NO149957B
NO149957B NO790031A NO790031A NO149957B NO 149957 B NO149957 B NO 149957B NO 790031 A NO790031 A NO 790031A NO 790031 A NO790031 A NO 790031A NO 149957 B NO149957 B NO 149957B
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methoxy
butan
naphthyl
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Carl John Rose
David Miller
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Beecham Group Ltd
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/20Unsaturated compounds containing keto groups bound to acyclic carbon atoms
    • C07C49/255Unsaturated compounds containing keto groups bound to acyclic carbon atoms containing ether groups, groups, groups, or groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/67Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
    • C07C45/673Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by change of size of the carbon skeleton
    • C07C45/676Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by change of size of the carbon skeleton by elimination of carboxyl groups

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
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Abstract

Fremgangsmåte for fremstilling av 4-(6metoksy-2naftyl)butan-2-on.Process for the preparation of 4- (6-methoxy-2-naphthyl) butan-2-one.

Description

Oppfinnelsen vedrører en fremgangsmåte for fremstilling av 4-(6<1->metoksy-2'-naftyl)butan-2-on. The invention relates to a process for the production of 4-(6<1->methoxy-2'-naphthyl)butan-2-one.

Britisk patent 1.474.377 åpenbarer blant annet at 4-(6'-metoksy-2'-naftyl)butan-2-on er i besittelse av nyttig anti-inflammatorisk aktivitet. En spesielt foretrukket fremgangsmåte er nå oppdaget som kan anvendes for fremstilling av denne forbindelse med spesielt godt utbytte. Denne fremgangsmåte er karakterisert ved hydrogenering av en forbindelse av formel (I) : hvor X og Y hver er hydrogenatomer eller danner sammen en dobbelt binding mellom karbonatomene som de er knyttet til; og R er en benzyl- eller substituert benzyl-gruppe méd formel (a), (b) eller (c), British patent 1,474,377 discloses, among other things, that 4-(6'-methoxy-2'-naphthyl)butan-2-one possesses useful anti-inflammatory activity. A particularly preferred method has now been discovered which can be used for the production of this compound with a particularly good yield. This method is characterized by hydrogenation of a compound of formula (I): where X and Y are each hydrogen atoms or together form a double bond between the carbon atoms to which they are linked; and R is a benzyl or substituted benzyl group with formula (a), (b) or (c),

hvor R 1 og R 2 uavhengig av hverandre er hydrogen eller halogenatomer eller lav-alkyl, lav-alkoksyl eller nitro, og hydrogeneringen foregår i et organisk løsningsmiddel. where R 1 and R 2 independently of each other are hydrogen or halogen atoms or lower alkyl, lower alkoxy or nitro, and the hydrogenation takes place in an organic solvent.

Enhver substituent R 1 eller R 2 som er til stede på en fenylring, er helst i para- eller meta-stilling. Halogenatomer er mer passende brom- eller kloratomer. Generelt er ikke mer enn én substituent R 1 eller R 2 til stede på fenylgruppen. Any substituent R 1 or R 2 present on a phenyl ring is preferably in the para or meta position. Halogen atoms are more appropriately bromine or chlorine atoms. In general, no more than one substituent R 1 or R 2 is present on the phenyl group.

Spesielt egnede grupper R inkluderer benzyl, p-metoksy-.i benzyl, p-brombenzyl, p-metylbenzyl og p-klorbenzyl. Particularly suitable groups R include benzyl, p-methoxy-1 benzyl, p-bromobenzyl, p-methylbenzyl and p-chlorobenzyl.

Én foretrukken gruppe R er benzylgruppen. One preferred group R is the benzyl group.

Hydrogeneringen av forbindelsen av formel (I) kan utføres ved anvendelse av et lavt, middels eller høyt hydrogentrykk, f.eks. fra 0,5 til 4 atm. hydrogen, men generelt, for å hindre over-reduksjon, foretrekkes det å anvende et trykk på 0,9-1,5 atm. hydrogen, f.eks. 1 atm. trykk. The hydrogenation of the compound of formula (I) can be carried out using a low, medium or high hydrogen pressure, e.g. from 0.5 to 4 atm. hydrogen, but in general, to prevent over-reduction, it is preferred to use a pressure of 0.9-1.5 atm. hydrogen, e.g. 1 atm. Print.

Hydrogeneringen vil bli utført i nærvær av en katalysator, f.eks. en edel-metall-katalysator, f.eks. palladium, som foretrekkes . Passende former av palladiumkatalysatorer inkluderer palladium på trekull, palladium på bariumsulfat eller palladium på kalsiumkarbonat. Andre edelmetall-katalysatorer som kan anvendes, inkluderer rhodium, f.eks. rhodium på aluminiumoksyd. Platina foretrekkes normalt ikke. The hydrogenation will be carried out in the presence of a catalyst, e.g. a noble metal catalyst, e.g. palladium, which is preferred. Suitable forms of palladium catalysts include palladium on charcoal, palladium on barium sulfate, or palladium on calcium carbonate. Other noble metal catalysts which may be used include rhodium, e.g. rhodium on aluminum oxide. Platinum is not normally preferred.

Egnede løsningsmidler for reaksjonen inkluderer lavere alkoholer, estere og halogenhydrokarboner og ketoniske løsnings-midler, f.eks. metylisobutylketon eller aceton. Spesielt egnede løsningsmidler inkluderer estere, f.eks. metylacetat og etylacetat hvorav etylacetat foretrekkes. Suitable solvents for the reaction include lower alcohols, esters and halohydrocarbons and ketone solvents, e.g. methyl isobutyl ketone or acetone. Particularly suitable solvents include esters, e.g. methyl acetate and ethyl acetate of which ethyl acetate is preferred.

Reaksjonen kan utføres ved nedsatt, omgivelses- eller forhøyet temperatur, f.eks. 0° til 35°C, og helst ved omgivel-sestemperatur . The reaction can be carried out at reduced, ambient or elevated temperature, e.g. 0° to 35°C, and preferably at ambient temperature.

Så snart reaksjonen er over (f.eks. fastslått ved TLC eller opphør av hydrogen-opptak) kan den ønskede forbindelse oppnås ved frafiltrering av katalysatoren og fjerning av løsningsmidlet, f.eks. ved inndampning under redusert trykk. As soon as the reaction is over (e.g. determined by TLC or cessation of hydrogen uptake) the desired compound can be obtained by filtering off the catalyst and removing the solvent, e.g. by evaporation under reduced pressure.

Om ønskes, kan således oppnådde forbindelse renses ytterligere ved rekrystallisasjon, f.eks. fra vandig etanol. If desired, the thus obtained compound can be further purified by recrystallization, e.g. from aqueous ethanol.

Hydrogeneringen av forbindelsen av formel (I) utføres for-trinnsvis på en forbindelse hvor X og Y representerer en dobbeltbinding sammen med den tilstedeværende C-C-binding, på bakgrunn av den bekvemme fremstilling av slike forbindelser ved omsetning av 6-metoksy-2-naftaldehyd med en forbindelse av formel The hydrogenation of the compound of formula (I) is preferably carried out on a compound where X and Y represent a double bond together with the C-C bond present, on the basis of the convenient preparation of such compounds by reacting 6-methoxy-2-naphthaldehyde with a compound of formula

(III): (III):

hvor R er som definert for formel (I). where R is as defined for formula (I).

Fordelene ved syntesen i henhold til oppfinnelsen fremfor den fremgangsmåte som anvender ikke-hydrogenolyserbare estere inkluderer (a) høyere totale utbytter; (b) ett reaksjonstrinn mindre, hvilket innebærer mindre håndtering av forbindelser og apparatur og mindre mulighet for dannelse av forurensninger, og (c) effektiv oppberedning. The advantages of the synthesis according to the invention over the process using non-hydrogenolizable esters include (a) higher overall yields; (b) one less reaction step, which means less handling of compounds and apparatus and less opportunity for the formation of contaminants, and (c) efficient preparation.

De følgende eksempler belyser oppfinnelsen, men først gjengis et sammenligningseksempel. The following examples illustrate the invention, but first a comparative example is reproduced.

Sammenligningseksempel Comparative example

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on under anvendelse av etylacetoacetat Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one using ethyl acetoacetate

6-metoksy-2-naftaldehyd (93,0 g, 0,5 mol), etylacetoacetat (71,5 g, 0,55 mol), cykloheksan (1,0 liter), piperidin (5,0 ml) og fenyleddiksyre (1,5 g) ble oppvarmet under tilbakeløp i 22 timer, idet vann ble fjernet under anvendelse av en Dean-Stark-apparatur. Løsningsmiddel ble fjernet under redusert trykk slik at man fikk rått 3-etoksykarbonyl-4-(6'-metoksy-2<1->naftyl)but-3-en-2-on (164,8 g) i form av en viskøs olje som ble anvendt direkte for neste trinn. 6-Methoxy-2-naphthaldehyde (93.0 g, 0.5 mol), ethyl acetoacetate (71.5 g, 0.55 mol), cyclohexane (1.0 L), piperidine (5.0 mL), and phenylacetic acid ( 1.5 g) was heated under reflux for 22 h, water being removed using a Dean-Stark apparatus. Solvent was removed under reduced pressure to give crude 3-ethoxycarbonyl-4-(6'-methoxy-2<1->naphthyl)but-3-en-2-one (164.8 g) as a viscous oil that was used directly for the next step.

Den viskøse olje (162,9 g) i etanol (1050 ml) ble hydrogenert ved romtemperatur og atmosfæretrykk i nærvær av 10 % palladium på trekull (15,0 g). Etter 5 1/2 timer var hydrogenopptaket fullstendig, og katalysatoren ble filtrert fra, vasket med 100 ml etanol og etanolfiltratene som inneholdt 3-etoksykarbonyl-4-(6<1->metoksy-2<1->naftyl)butan-2-on ble anvendt i neste trinn. The viscous oil (162.9 g) in ethanol (1050 mL) was hydrogenated at room temperature and atmospheric pressure in the presence of 10% palladium on charcoal (15.0 g). After 5 1/2 hours the hydrogen uptake was complete and the catalyst was filtered off, washed with 100 ml of ethanol and the ethanol filtrates containing 3-ethoxycarbonyl-4-(6<1->methoxy-2<1->naphthyl)butane-2- on was used in the next step.

90 % av det ovennevnte filtrat (dvs. som inneholdt 0,45 mol produkt under antagelse av 100 % omsetning) (1200 ml) og 5n HC1 (470 ml) ble tilbakeløpsbehandlet i 7 timer. Fjerning av etanol under redusert trykk ga et lærfarvet fast stoff som ble oppløst i 1,0 liter etylacetat. Vannskiktet ble separert og vasket med mer etylacetat (10 0 ml). De kombinerte organiske løsninger ble vasket med natriumbikarbonatløsning til pH 8 90% of the above filtrate (ie containing 0.45 mol of product assuming 100% conversion) (1200 mL) and 5N HCl (470 mL) were refluxed for 7 hours. Removal of ethanol under reduced pressure gave a leather colored solid which was dissolved in 1.0 L of ethyl acetate. The aqueous layer was separated and washed with more ethyl acetate (100 mL). The combined organic solutions were washed with sodium bicarbonate solution to pH 8

(800 ml), vann og tørket (Na2S04). (800 ml), water and dried (Na 2 SO 4 ).

Fjerning av løsningsmiddel under redusert trykk ga et lærfarvet, fettaktig fast stoff (103,6 g) som ble krystallisert ut fra 80 % etanol/vann (588 ml) og deretter etanol (275 ml) slik at man fikk 4-(6<1->metoksy-2<1->naftyl)-butan-2-on (55,9 g, 54,5 %) smp. 80,5-81°. Removal of solvent under reduced pressure gave a leather-colored, oily solid (103.6 g) which was crystallized from 80% ethanol/water (588 mL) and then ethanol (275 mL) to give 4-(6<1 ->methoxy-2<1->naphthyl)-butan-2-one (55.9 g, 54.5%) m.p. 80.5-81°.

Reaksjoner i større målestokk (med 27 mol 6-metoksy-2-naftaldehyd) har resultert i meget mindre totale utbytter (3 7-41 %) av sluttproduktet. Reactions on a larger scale (with 27 mol of 6-methoxy-2-naphthaldehyde) have resulted in much lower total yields (37-41%) of the final product.

Eksempel 1 Example 1

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on under anvendelse av benzylacetoacetat Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one using benzyl acetoacetate

Utgangsmateriale Source material

6-metoksy-2-naftaldehyd (37,2 g, 0,2 mol), benzylacetoacetat (40,0 g, 0,21 mol) cykloheksan (500 ml) og piperidiniumacetat (2,0 g) ble tilbakeløpsbehandlet i 4 timer, idet vann ble fjernet med en Dean-Stark-apparatur. Eter (250 ml) ble tilsatt og blandingen avkjølt til 5° i 16 timer slik at man fikk 3-benzyloksykarbonyl-4-(6'-metoksy-2<1->naftyl)but-3-en-2-on (58,0 g, 80,6 %) smp. 88-90° i form av et gult fast stoff. Dette ble ikke renset ytterligere, men ble anvendt direkte i det neste trinn. 6-Methoxy-2-naphthaldehyde (37.2 g, 0.2 mol), benzyl acetoacetate (40.0 g, 0.21 mol), cyclohexane (500 mL) and piperidinium acetate (2.0 g) were refluxed for 4 h, as water was removed with a Dean-Stark apparatus. Ether (250 mL) was added and the mixture cooled to 5° for 16 h to give 3-benzyloxycarbonyl-4-(6'-methoxy-2<1->naphthyl)but-3-en-2-one (58 .0 g, 80.6 %) m.p. 88-90° in the form of a yellow solid. This was not purified further, but was used directly in the next step.

3-benzyloksykarbonyl-4-(6<1->metoksy-2'-naftyl)but-3-en-2-on (58,0 g) ble rystet med 10% palladisert trekull (4,0 g) i 500 ml etylacetat under hydrogen inntil reaksjonen var ferdig. Fjerning av katalysator ved filtrering fulgt av inndampning av filtratet ga et hvitt, fast stoff (36,0 g) som ble rekrystallisert ut fra 80% etanol/vann (200 ml) slik at man fikk 4-(6 *-metoksy-2'-naftyl)butan-2-on [30,6 g, 83,3% (totalt utbytte fra aldehyd 6 7,1%] smp. 81°. 3-Benzyloxycarbonyl-4-(6<1->methoxy-2'-naphthyl)but-3-en-2-one (58.0 g) was shaken with 10% palladium charcoal (4.0 g) in 500 ml ethyl acetate under hydrogen until the reaction was complete. Removal of catalyst by filtration followed by evaporation of the filtrate gave a white solid (36.0 g) which was recrystallized from 80% ethanol/water (200 mL) to give 4-(6*-methoxy-2' -naphthyl)butan-2-one [30.6 g, 83.3% (total yield from aldehyde 6 7.1%] mp 81°.

Reaksjoner i større målestokk (med 20 mol 6-metoksy-2-naftaldehyd) opprettholdt det totale utbytte på 67% slutt-produkt . Reactions on a larger scale (with 20 mol of 6-methoxy-2-naphthaldehyde) maintained the overall yield of 67% final product.

Eksempel 2 Example 2

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one

Hydrogeneringen som ble beskrevet i eksempel 1 ble gjentatt under anvendelse av de alternative løsningsmidler metylacetat, aceton og metylisobutylketon (MIBK). Hydrogenering ble utført inntil opptaket var komplett. Resultatene var som følger: The hydrogenation described in Example 1 was repeated using the alternative solvents methyl acetate, acetone and methyl isobutyl ketone (MIBK). Hydrogenation was carried out until the absorption was complete. The results were as follows:

Eksempel 3 Example 3

Fremstilling av 4-( 6 ' - métoksy- 2 ' - naf tyl) butan- 2- on Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one

Hydrogeneringen som er beskrevet i eksempel 1, ble gjentatt under anvendelse av den alternative katalysator 5 % rhodium på aluminiumoksyd. Det ble funnet at det teoretiske opptak av hydrogen krevet 2 8 timer og at utbyttet som ble opp-nådd, var 75 %. The hydrogenation described in Example 1 was repeated using the alternative catalyst 5% rhodium on alumina. It was found that the theoretical uptake of hydrogen required 28 hours and that the yield achieved was 75%.

Eksempel 4 Example 4

Fremstilling av utgangsmateriale Production of starting material

p-metylbenzylacetoacetat (18,0 g, 0,0874 mol), 6-metoksy-2-naftaldehyd (14,8 g, 0,0796 mol), cykloheksan (200 ml) og en katalytisk mengde av piperidiniumacetat (0,8 g) ble til-bakeløpsbehandlet sammen i 2,5 timer og vannet oppsamlet i en Dean og Stark-mottager. 170 ml eter ble tilsatt, blandingen ble avkjølt til -5°, og man fikk 10,7 g av forbindelsen 3-p-metylbenzyloksykarbonyl-4-(6<1->metoksy-2'-naftyl)but-3-en-2-on (forbindelse A) i 36% utbytte. Ytterligere utbytter ble isolert ved avkjøling og ved konsen-trasjon og krystallisasjon ut fra eter slik at man til slutt fikk i alt 22,6 g av forbindelse A i 75,9% utbytte, i form av et gult fast stoff, smp. 78-80°. p-methylbenzylacetoacetate (18.0 g, 0.0874 mol), 6-methoxy-2-naphthaldehyde (14.8 g, 0.0796 mol), cyclohexane (200 mL) and a catalytic amount of piperidinium acetate (0.8 g ) were refluxed together for 2.5 h and the water collected in a Dean and Stark receiver. 170 ml of ether were added, the mixture was cooled to -5°, and 10.7 g of the compound 3-p-methylbenzyloxycarbonyl-4-(6<1->methoxy-2'-naphthyl)but-3-en- 2-on (compound A) in 36% yield. Further yields were isolated by cooling and by concentration and crystallization from ether so that a total of 22.6 g of compound A was finally obtained in 75.9% yield, in the form of a yellow solid, m.p. 78-80°.

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one

Forbindelse A (5 g, 0,0134 mol), 10% palladium på trekull (0,25 g) og etylacetat (30 ml) ble rystet sammen under hydrogen-atmosfære inntil hydrogenopptaket hadde avtatt. Fjerning av katalysatoren ved filtrering og løsningsmidlet ved fordampning ga et hvitt, fast stoff som ble rekrystallisert ut fra etanol (15 ml) slik at man i to omganger fikk et totalt utbytte på 2,6 g 4-(6'-metoksy-2<1->naftyl)butan-2-on (85,3 %) i form av et hvitt, fast stoff, smp. 78,5-80°. Det totale utbytte fra 6-metoksy-2-naftaldehyd til 4-(6',metoksy-2'-naftyl)butan-2-on under anvendelse av p-metylbenzylacetoacetat var 64,7 %. Compound A (5 g, 0.0134 mol), 10% palladium on charcoal (0.25 g) and ethyl acetate (30 ml) were shaken together under a hydrogen atmosphere until hydrogen uptake had subsided. Removal of the catalyst by filtration and the solvent by evaporation gave a white solid which was recrystallized from ethanol (15 ml) to give a total yield of 2.6 g of 4-(6'-methoxy-2< 1->naphthyl)butan-2-one (85.3%) in the form of a white solid, m.p. 78.5-80°. The overall yield from 6-methoxy-2-naphthaldehyde to 4-(6',methoxy-2'-naphthyl)butan-2-one using p-methylbenzylacetoacetate was 64.7%.

[p-metylbenzylacetoacetatet ble fremstilt på følgende måte : Etylacetoacetat (22,5 g, 0,173 mol) og p-metylbenzyl-. alkohol (18,3 g, 0,15 mol) ble oppvarmet sammen ved ca. 200° [p-Methylbenzylacetoacetate was prepared as follows: Ethyl acetoacetate (22.5 g, 0.173 mol) and p-methylbenzyl-. alcohol (18.3 g, 0.15 mol) was heated together at ca. 200°

og den frigjorte etanol oppsamlet ved destillasjon. Reaksjonsblandingen ble deretter destillert fraksjonert, idet slutt-fraksjonen som kokte med en topptemperatur på 118-122° ved 1,0 mmHg var p-metylbenzylacetoacetat. (Utbytte 26g)]. and the liberated ethanol collected by distillation. The reaction mixture was then fractionally distilled, the final fraction boiling with a peak temperature of 118-122° at 1.0 mmHg being p-methylbenzyl acetoacetate. (Yield 26g)].

Eksempel 5 Example 5

Fremstilling av utgangsmateriale Production of starting material

p-metoksybenzylacetoacetat (25 g 0,1126 mol), 6-metoksy-2-naftaldehyd (18,6 g 0,1 mol), cykloheksan (200 ml) p-Methoxybenzylacetoacetate (25 g 0.1126 mol), 6-methoxy-2-naphthaldehyde (18.6 g 0.1 mol), cyclohexane (200 mL)

og piperidiniumacetat (1 g) ble tilbakeløpsbehandlet sammen i 1,5 timer og vannet oppsamlet i en Dean og Stark-mottager. and piperidinium acetate (1 g) were refluxed together for 1.5 h and the water collected in a Dean and Stark receiver.

200 ml eter ble tilsatt, og den utfelte olje fikk krystallisere natten over slik at man fikk 31 g (79,5 %) av 3-p-metoksYbenzyl-oksykarbonyl-4-(6<1->metoksy-2<1->naftyl)but-3-en-2-on (forbindelse A) i form av et gult, fast stoff, smp. 93,5-95,5°. 200 ml of ether was added, and the precipitated oil was allowed to crystallize overnight to give 31 g (79.5%) of 3-p-methoxybenzyl-oxycarbonyl-4-(6<1->methoxy-2<1-> naphthyl)but-3-en-2-one (compound A) in the form of a yellow solid, m.p. 93.5-95.5°.

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one

5 q av forbindelse A ble hydrogenert som angitt i eksempel 4 slik at man fikk 2,3 g, (78,7 %) av 4- (6 ' -met-oksy-2 ' -naf tyl) - butan-2-on i form av et hvitt, fast stoff, smp. 78,5-80°. 5 q of compound A was hydrogenated as indicated in Example 4 to give 2.3 g, (78.7%) of 4-(6'-meth-oxy-2'-naphthyl)-butan-2-one in the form of a white solid, m.p. 78.5-80°.

Det totale utbytte fra 6-metoksy-2-naftaldehyd til 4-(6'-metoksy-2'-naftyl)butan-2-on under anvendelse av p-metoksybenzylacetoacetat var 62,6 %. The overall yield from 6-methoxy-2-naphthaldehyde to 4-(6'-methoxy-2'-naphthyl)butan-2-one using p-methoxybenzylacetoacetate was 62.6%.

[p-metoksybenzylacetoacetatet ble fremstilt på The [p-methoxybenzylacetoacetate was prepared on

følgende måte: the following way:

p-metoksybenzylalkohol (27,6 g 0,2 mol) og etylacetoacetat (32 g, 0,246 mol) ble oppvarmet sammen til ca. p-Methoxybenzyl alcohol (27.6 g, 0.2 mol) and ethyl acetoacetate (32 g, 0.246 mol) were heated together to approx.

190° og den etanol som således dannet seg, oppsamlet ved destillasjon. Reaksjonsblandingen ble fraksjonert destillert og p-metoksybenzylacetoacetat oppsamlet ved en topptemperatur på 126-132° og et vakuum på 0,3 mmHg. Utbytte: 39 g (87,7 %)]. 190° and the ethanol thus formed collected by distillation. The reaction mixture was fractionally distilled and p-methoxybenzylacetoacetate collected at a peak temperature of 126-132° and a vacuum of 0.3 mmHg. Yield: 39 g (87.7%)].

Eksempel 6 Example 6

Fremstilling av utgangsmateriale Production of starting material

Benzhydrylacetoacetat (9 g, 0,0336 mol), 6-metoksy-2-naftaldehyd (5 g, 0,0269 mol), cykloheksan (80 ml) og piperidiniumacetat (0,26 g) ble tilbakeløpsbehandlet sammen i 1,5 timer og vannet oppsamlet i en Dean og Stark-mottager. 6 0 ml eter ble tilsatt og blandingen avkjølt til 0° slik at man fikk 9,4 g (80%) av benzhydryloksykarbonyl-4-(6<1->metoksy-2-naftyl)-but-3-en-2-on (forbindelse B) i to omganger, smp. 124-126°. Benzhydrylacetoacetate (9 g, 0.0336 mol), 6-methoxy-2-naphthaldehyde (5 g, 0.0269 mol), cyclohexane (80 mL) and piperidinium acetate (0.26 g) were refluxed together for 1.5 h and the water collected in a Dean and Stark receiver. 60 ml of ether was added and the mixture cooled to 0° to give 9.4 g (80%) of benzhydryloxycarbonyl-4-(6<1->methoxy-2-naphthyl)-but-3-en-2- on (compound B) in two portions, m.p. 124-126°.

Fremstilling av 4-( 6'- metoksy- 2'- naftyl) butan- 2- on Preparation of 4-(6'-methoxy-2'-naphthyl)butan-2-one

5 g (0,0115 mol) av forbindelse B ble hydrogenert som angitt i eksempel 4, slik at man fikk 2,1 g (80,3%) av 4-(6'-metoksy-2-naftyl)butan-2-on i form av et hvitt, fast stoff, smp. 79-80,5°. Totalt utbytte fra 6-metoksy-2-naft-<!>. aldehyd til 4-(6'-metoksy-2-naftyl)butan-2-on under anvendelse av benzhydrylacetoacetat er 64,2%. 5 g (0.0115 mol) of compound B was hydrogenated as indicated in Example 4, so that 2.1 g (80.3%) of 4-(6'-methoxy-2-naphthyl)butane-2- on in the form of a white solid, m.p. 79-80.5°. Total yield from 6-methoxy-2-naphth-<!>. aldehyde to 4-(6'-methoxy-2-naphthyl)butan-2-one using benzhydrylacetoacetate is 64.2%.

[Benzhydrylacetoacetatet ble fremstilt på følgende måte : [The benzhydrylacetoacetate was prepared as follows:

Benzhydrol (20 g, 0,1087 mol) og etylacetoacetat Benzhydrol (20 g, 0.1087 mol) and ethyl acetoacetate

(13 g, 0,1 mol) ble oppvarmet sammen til 170° og den etanol som således dannet seg, fjernet ved destillasjon. Fraksjonert destillasjon ved 1,0 mmHg ga 10,5 g (39 %) benzhydrylacetoacetat i form av en farveløs væske som senere stivnet, smp. 44-54°]. (13 g, 0.1 mol) were heated together to 170° and the ethanol thus formed removed by distillation. Fractional distillation at 1.0 mmHg gave 10.5 g (39%) of benzhydrylacetoacetate as a colorless liquid which later solidified, m.p. 44-54°].

Claims (5)

1. Fremgangsmåte for fremstilling av 4-(6'-metoksy-2'-naftyl)-butan-2-on, karakterisert ved at man hydro-generer en forbindelse av formel (I): hvor X og Y betyr hydrogen eller sammen og med den tilstedeværende C-C-binding utgjør en dobbeltbinding og R er benzyl eller substituert benzyl med formel hvor R' 1 og R 2 uavhengig av hverandre betyr hydrogen, halogen, lavere alkyl, lavere alkoksy, eller nitro, i et organisk løs-ningsmiddel .1. Process for the production of 4-(6'-methoxy-2'-naphthyl)-butan-2-one, characterized by hydrogenating a compound of formula (I): where X and Y mean hydrogen or together and with the C-C bond present constitute a double bond and R is benzyl or substituted benzyl of formula where R' 1 and R 2 independently of each other mean hydrogen, halogen, lower alkyl, lower alkoxy, or nitro, in an organic solvent. 2. Fremgangsmåte som angitt i krav 1, karakterisert ved at det hydrogeneres en forbindelse hvor R er en benzylgruppe.2. Method as stated in claim 1, characterized in that a compound is hydrogenated where R is a benzyl group. 3. Fremgangsmåte som angitt i krav 1 eller 2, karakterisert ved at man anvender en forbindelse av formel (I) hvor X og Y sammen og med den tilstedeværende C-C-binding danner en dobbeltbinding.3. Method as stated in claim 1 or 2, characterized in that a compound of formula (I) is used where X and Y together and with the present C-C bond form a double bond. 4. Fremgangsmåte som angitt i hvilket som helst av kravene 1 til 3, karakterisert ved at hydrogeneringen utføres under anvendelse av et hydrogentrykk på 0,9-1,5 atm. i nærvær av en edelmetallkatalysator.4. Method as stated in any one of claims 1 to 3, characterized in that the hydrogenation is carried out using a hydrogen pressure of 0.9-1.5 atm. in the presence of a noble metal catalyst. 5. Fremgangsmåte som angitt i krav 4, karakterisert ved at det som metall anvendes palladium.5. Method as stated in claim 4, characterized in that palladium is used as metal.
NO790031A 1978-01-07 1979-01-05 PROCEDURE FOR THE PREPARATION OF 4- (6`-METOXY-2`-NAPHYL) BUTAN-2-ON. NO149957C (en)

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